EP0002122A1 - Method and apparatus for separating paper and fibres from portions of polyethylene film material - Google Patents
Method and apparatus for separating paper and fibres from portions of polyethylene film material Download PDFInfo
- Publication number
- EP0002122A1 EP0002122A1 EP19780300612 EP78300612A EP0002122A1 EP 0002122 A1 EP0002122 A1 EP 0002122A1 EP 19780300612 EP19780300612 EP 19780300612 EP 78300612 A EP78300612 A EP 78300612A EP 0002122 A1 EP0002122 A1 EP 0002122A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- polyethylene film
- paper
- portions
- balls
- fibres
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B11/00—Arrangement of accessories in apparatus for separating solids from solids using gas currents
- B07B11/06—Feeding or discharging arrangements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B1/00—Conditioning for facilitating separation by altering physical properties of the matter to be treated
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B9/00—General arrangement of separating plant, e.g. flow sheets
- B03B9/06—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse
- B03B9/061—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse the refuse being industrial
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents
- B07B7/01—Selective separation of solid materials carried by, or dispersed in, gas currents using gravity
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents
- B07B7/04—Selective separation of solid materials carried by, or dispersed in, gas currents by impingement against baffle separators
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B9/00—Combinations of apparatus for screening or sifting or for separating solids from solids using gas currents; General arrangement of plant, e.g. flow sheets
- B07B9/02—Combinations of similar or different apparatus for separating solids from solids using gas currents
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
- B29B17/02—Separating plastics from other materials
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- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/02—Pretreatment of the raw materials by chemical or physical means
- D21B1/026—Separating fibrous materials from waste
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/02—Pretreatment of the raw materials by chemical or physical means
- D21B1/026—Separating fibrous materials from waste
- D21B1/028—Separating fibrous materials from waste by dry methods
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21B—FIBROUS RAW MATERIALS OR THEIR MECHANICAL TREATMENT
- D21B1/00—Fibrous raw materials or their mechanical treatment
- D21B1/04—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres
- D21B1/12—Fibrous raw materials or their mechanical treatment by dividing raw materials into small particles, e.g. fibres by wet methods, by the use of steam
- D21B1/30—Defibrating by other means
- D21B1/32—Defibrating by other means of waste paper
- D21B1/322—Defibrating by other means of waste paper coated with synthetic materials
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2023/00—Use of polyalkenes or derivatives thereof as moulding material
- B29K2023/04—Polymers of ethylene
- B29K2023/06—PE, i.e. polyethylene
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2711/00—Use of natural products or their composites, not provided for in groups B29K2601/00 - B29K2709/00, for preformed parts, e.g. for inserts
- B29K2711/12—Paper, e.g. cardboard
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2007/00—Flat articles, e.g. films or sheets
- B29L2007/008—Wide strips, e.g. films, webs
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2009/00—Layered products
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2031/00—Other particular articles
- B29L2031/712—Containers; Packaging elements or accessories, Packages
- B29L2031/7158—Bottles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
- B29L2031/00—Other particular articles
- B29L2031/712—Containers; Packaging elements or accessories, Packages
- B29L2031/7162—Boxes, cartons, cases
- B29L2031/7166—Cartons of the fruit juice or milk type, i.e. containers of polygonal cross sections formed by folding blanks into a tubular body with end-closing or contents-supporting elements, e.g. gable type containers
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/52—Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/64—Paper recycling
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/80—Packaging reuse or recycling, e.g. of multilayer packaging
Definitions
- the present invention relates to a method and apparatus for separating paper fibres from portions of polyethylene film in order to obtain a useful, recyclable polyethylene product.
- polyethylene film is frequently laminated to one or both sides of a paper substrate and the resulting laminated material is used for a wide variety of purposes.
- the present invention proposes to accomplish the separation of the paper fibres from the polyethylene film pieces by a method and apparatus which will produce a polyethylene product of acceptable purity for recycling purposes and may, in addition, enable the remaining paper fibres to be recovered as a usable product.
- film comprising a shredding device for converting said polyethylene sheet/ paper fibre to substantially uniform balls of paper fibre and small portions of polyethylene film, the uniform balls of paper fibre having an average diameter of about 2 mm; an air blower for entraining said balls and film portions in a stream of air and projecting them along a predetermined pathway; a first plurality of impact surfaces in said pathway to impact said paper fibre balls and polyethylene film to strip said paper fibres from said polyethylene film portions; a cascade of-separators having alternate high velocity passages and low velocity chambers in series to provide air entrainment of said polyethylene film portions while allowing said paper balls to fall out in the low velocity chambers, a screen defining a bottom wall for said cascade of separators; gravity collection chambers beneath the screens of each of said low velocity chambers to receive the denser, damp paper fibre balls that fall out through the screen in said low velocity chamber; means to remove the paper fibre balls
- a method of separating paper fibres from portions of polyethylene film characterised by the steps of beating portions of polyethylene film contaminated with dampened paper fibres into a mixture of polyethylene film portions and balls cf paper fibre, blowing the said mixture against a plurality of impact surfaces, and therefrom through'an alternating series of high velocity passages and low velocity chambers . such that the paper fibre balls fall out of the stream in the low velocity chambers, collecting the paper fibre balls below the low velocity chambers, and collecting the polyethylene film portions downstream of the said series.
- FIG. 1 the drawing schematically illustrates a device 10 identified by the legend -SHREDDER- which is a commercially available device manufactured in the United States of America by Bolton-Emerson, Inc. of 9, Osgood Street, Lawrence, Massachusetts 01842 and sold under the trade mark ZE R G L OMAT.
- This device functions somewhat in the manner of a domestic kitchen blender and comprises an outer cylindrical casing having, within it, a rotating blade 11 mounted about a vertical axis 12 and driven by an electric motor 13.
- the feedstock for the shredder is the product of a hydro-pulper and comprises pieces of polyethylene film of a variety of sizes which are contaminated by paper fibres.
- the feedstock, as it is received from the hydro-pulper, contains a substantial amount of water and at least some of this water is, desirably, removed from the feedstock before it is placed in the shredder.
- the removal of the water may be accomplished by any of a variety of means which will readily occur to those skilled in the art.
- the feedstock may be passed through rollers to squeeze out excess water, the feedstock may be centrifugally treated or the water may be removed in other ways.
- the feedstock that is placed in the shredder is, however, sufficiently damp for the paper fibres to contain a proportion of water sufficient to make their specific gravity greater than that of the polyethylene film for reasons that will be apparent later in this description.
- the shredder operates in a "batch” fashion and when charged with feedstock, and energized, converts the feedstock to substantially uniformly sized balls of paper fibre from which the polyethylene pieces have been largely stripped by impact with the rotating blades.
- the average diameter of the "balis” is about 2 mm.
- the "balls" of damp paper fibre are of relatively higher density than the pieces of polyethylene film and are, accordingly, susceptible to gravity separation by air entrainment since, being small and relatively denser, they tend to fall out of the air stream while the lightar pieces of polyethylene film, having high air resistance and, accordingly, high air entrainment ability are passed through the apparatus to be recovered at the downstream end.
- the fluffer 17 is seen to comprise an outer housing which is provided with an entrance aperture 18 which, in one embodiment of the invention, may conveniently have a diameter of something between 25 and 26 cm.
- the air entrained polyethylene film/paper fibre balls impacts against a first plurality of impact surfaces which bear reference numerals 19 to 27 inclusive in Figures 2 and 3 and all of which lie at an angle of less than 900 to the stream of air.
- the function of the first plurality of impact surfaces is to complete, by physical impact, the separation of the polyethylene film from the paper fibres and this is accomplished by causing the material to impact against the angularly disposed impact surfaces in a more or less random, highly turbulent manner.
- the relatively high velocity air stream in which the material is entrained assists in this separation due to the difference between the specific gravity of the damp paper fibre balls and the polyethylene film.
- the relatively low air resistance of the paper fibre balls and the relatively high air resistance of the polyethylene film pieces aids in this separation.
- An exit passage 23 is provided from the chamber defined by the fluffer 17 and leads into the first of the cascade of separator chambers which are identified in Figure 1 by the legend -SEPARATORS- and by reference numerals 29.
- Each separator chamber 29 is.as illustrated in Figure 4, and comprises a generally rectangular chamber, the first in the cascade having a rectangular entrance aperture 30 and a chevron shaped exit aperture 31.
- each separator chamber is to provide alternate passages of high velocity (the entrance and exit apertures) and chambers of low velocity (the interior of each separator chamber 29) so as to enable the relatively heavier damp paper fibre balls to fall by gravity through a screen 32 into'a qravity collection chamber 33 located beneath the screen.
- each separator chamber 29 is provided with a transparent window 34 through which the activity within the chamber may be observed.
- the provision of the transparent window is optional and is not an essential feature of the invention.
- each separator chamber may be provided with an openable access door 35 to provide access to the interior of the chamber for any of a variety of purposes that will readily be apparent.
- the screen 32 in the first series of the cascade of separators will be of a mesh approximately 1 cm and will be formed in 2 sections, separated by a dividing line 32a so as to enable the .screen to be removed through the access door 35.
- each collector chamber 33 Periodically, a discharge opening in the bottom of each collector chamber 33 will be opened to permit the accumulated paper fibre balls to fall downwardly to a point of collection which may be accomplished by any of several conventional means such as conveyors or the like.
- One convenient way of providing for the intermittent opening of the discharge opening in the bottom of the collection chamber 33 is to provide a spherical plug 36 which seats in a circular opening in the bottom of the collection chamber 33 and which may be intermittently lifted off its seat to permit the accumulated paper fibre balls to fall out through the discharge opening.
- a bridging member 50 extends across the upper portion of each collector chamber 33 and, at each end, is secured to the wall of the collector chamber 33 by means of a small flange 51 which may be spot welded to the wall.
- the lower surface of the member 50 carries a brafket 52 which, in turn, carries a pulley 53 over which is entrained a wire 54 which is connected, at one end, to the spherical plug 36 and, at its other end, is connected to the upper end 55 of an arm 56 which is pivotally mounted at 57 on standing structure 58 of the apparatus.
- a longitudinal shaft 59 carries a radial cam 60.
- the cam 60 engages the arm 56 and causes it to move to the dotted line position 56a as a result of which the wire 54 is pulled and the ball 36 is lifted off its seat to assume the dotted line position 36a.
- the radial dimension of the cam 6 0 will determine the height to which the spherical plug 36 is lifted, and the speed of rotation of the shaft 59 will determine the frequency at which it is lifted. It will be understood that there will be a plurality of cams 60 equal to the number of collection chambers 33 and it will also be appreciated that the cams 60 can be arranged on the shaft with the same angular orientation so that all spherical plugs are lifted at the same time or they may be arranged at different angular orientations relative to the shaft so that the spherical plugs are lifted sequentially in any desired order. Furthermore, the radial extent of the cams 60 may vary so that the spherical plugs are lifted by different amounts as may be desired.
- the air entrained material Having passed through the first five separators of the cascade, the air entrained material enters a second fluffer 37 constructed in a manner identical to the fluffer 17 illustrated in greater detail in Figures 2 and 3.
- a second plurality of impact surfaces takes place to further promote the physical separation of the polyethylene film from the damp paper fibre balls and, exiting from the second fluffer, the material passes through the second series of the cascade of separators identified by reference numeral 39.
- the air stream leaves the final exit 40 of the last of the cascade of separator chambers, it will contain substantially pure polyethylene film and, at this point, it may be collected, passed to a dryer 41 in which, by conventional means, the moisture content may be reduced to the desired level and, from the dryer,.the polyethylene film may be passed to an extruder 42 or to such other component of the apparatus as will produce a polyethylene product, suitable for recycling, in a form that can be readily shipped.
- the polyethylene film may be bagged, bailed, boxed or otherwise dealt with or, as illustrated in Figure 1, may be extruded into pellets, rods, bars or the like for shipment to a point of further use.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Wood Science & Technology (AREA)
- Environmental & Geological Engineering (AREA)
- Paper (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Artificial Filaments (AREA)
Abstract
Description
- The present invention relates to a method and apparatus for separating paper fibres from portions of polyethylene film in order to obtain a useful, recyclable polyethylene product.
- In modern day packaging, polyethylene film is frequently laminated to one or both sides of a paper substrate and the resulting laminated material is used for a wide variety of purposes.
- One of the industries making a very substantial use of a product of this kind is the dairy industry which uses the product to make containers for milk, cream and the like. The manufacture of, for example, milk cartons from large sheets of paper laminated with polyethylene film on one or both sides is accomplished by cutting the large sheets into blanks of predetermined form and assembling them by methods which are well known in the art. The process results in the production of a substantial quantity of scrap material which is useless for recycling as a paper product since it is contaminated with polyethylene and is useless for recycling as a polyethylene prodact since it is contaminated with paper.
- Current methods of attempting to recycle this material involve the passage of the scrap material through a device, well known in the ert, known as a hydro-pulper which, in the presence of large quantities of water, either with or without other additives, causes a substantial separation of paper fibres from the polyethylene film and enables the paper fibres entrained in the water to be recovered to a substantial degree for recycling purposes. However, the polyethylene film which is a product of the hydro-pulper operation is still a virtually useless product because the separation from the paper fibres is incomplete and the polyethylene film, being contaminated by an unacceptably high level of paper fibres is useless as a recycling product.
- Other operating methods and apparatuses, not necessarily for separating paper fibres from polyethylene, are described in United States Patent Specifications 4000031, 3836085, 3443687 and 3250389.
- Hitherto, it has not been possible to conveniently, economically and practically, separate the remaining paper fibres from the polyethylene film to produce a polyethylene film which is sufficiently free of paper fibre contamination to be acceptable as a usable polyethylene product.
- The present invention proposes to accomplish the separation of the paper fibres from the polyethylene film pieces by a method and apparatus which will produce a polyethylene product of acceptable purity for recycling purposes and may, in addition, enable the remaining paper fibres to be recovered as a usable product.
- According to one aspect of the invention, there is provided apparatus for stripping damp paper fibres from portions of polyethylene . film comprising a shredding device for converting said polyethylene sheet/ paper fibre to substantially uniform balls of paper fibre and small portions of polyethylene film, the uniform balls of paper fibre having an average diameter of about 2 mm; an air blower for entraining said balls and film portions in a stream of air and projecting them along a predetermined pathway; a first plurality of impact surfaces in said pathway to impact said paper fibre balls and polyethylene film to strip said paper fibres from said polyethylene film portions; a cascade of-separators having alternate high velocity passages and low velocity chambers in series to provide air entrainment of said polyethylene film portions while allowing said paper balls to fall out in the low velocity chambers, a screen defining a bottom wall for said cascade of separators; gravity collection chambers beneath the screens of each of said low velocity chambers to receive the denser, damp paper fibre balls that fall out through the screen in said low velocity chamber; means to remove the paper fibre balls from the collection chambers, and means to collect the polyethylene portions at the downstream end of the cascade of separators.
- According to another aspect of the invention, there is provided a method of separating paper fibres from portions of polyethylene film, the method characterised by the steps of beating portions of polyethylene film contaminated with dampened paper fibres into a mixture of polyethylene film portions and balls cf paper fibre, blowing the said mixture against a plurality of impact surfaces, and therefrom through'an alternating series of high velocity passages and low velocity chambers . such that the paper fibre balls fall out of the stream in the low velocity chambers, collecting the paper fibre balls below the low velocity chambers, and collecting the polyethylene film portions downstream of the said series.
- The invention will now be described in more detail, solely by way of example, with reference to the accompanying drawings, in which:-
- Figure 1 is an overall schematic view of an apparatus, in. side elevation, adapted to carry out the present invention;
- Figure 2 is a perspective view, with the cover removed, of the component of'Figure 1 identified by the legend -FLUFFER-;
- Figure 3 is a perspective view, partly cut away, of the device of Figure 2 taken from a different position;
- Figure 4 is an enlarged view, partly broken away, of one of the elements of Figure 1 identified by the legend -SEPARATORS-; and
- Figure 5 is an end elevation, partly in section, of one of the elements of Figure 1 identified by the legend -SEPARATORS-, showing a plug lifting mechanism.
- Referring now in detail to Figure 1, the drawing schematically illustrates a
device 10 identified by the legend -SHREDDER- which is a commercially available device manufactured in the United States of America by Bolton-Emerson, Inc. of 9, Osgood Street, Lawrence, Massachusetts 01842 and sold under the trade mark ZERGLOMAT. This device functions somewhat in the manner of a domestic kitchen blender and comprises an outer cylindrical casing having, within it, a rotatingblade 11 mounted about avertical axis 12 and driven by anelectric motor 13. - The feedstock for the shredder is the product of a hydro-pulper and comprises pieces of polyethylene film of a variety of sizes which are contaminated by paper fibres. The feedstock, as it is received from the hydro-pulper, contains a substantial amount of water and at least some of this water is, desirably, removed from the feedstock before it is placed in the shredder. The removal of the water may be accomplished by any of a variety of means which will readily occur to those skilled in the art. The feedstock may be passed through rollers to squeeze out excess water, the feedstock may be centrifugally treated or the water may be removed in other ways. The feedstock that is placed in the shredder is, however, sufficiently damp for the paper fibres to contain a proportion of water sufficient to make their specific gravity greater than that of the polyethylene film for reasons that will be apparent later in this description.
- The shredder operates in a "batch" fashion and when charged with feedstock, and energized, converts the feedstock to substantially uniformly sized balls of paper fibre from which the polyethylene pieces have been largely stripped by impact with the rotating blades. The average diameter of the "balis" is about 2 mm. The "balls" of damp paper fibre are of relatively higher density than the pieces of polyethylene film and are, accordingly, susceptible to gravity separation by air entrainment since, being small and relatively denser, they tend to fall out of the air stream while the lightar pieces of polyethylene film, having high air resistance and, accordingly, high air entrainment ability are passed through the apparatus to be recovered at the downstream end.
- After treatment in the shredder, the contents thereof are discharged through a
conduit 14 and entrained in a stream of air developed by ablower 15 and directed horizontally in the direction of anarrow 16 into .a fluffer which is indicated generally bereference numeral 17 in Figure 1. - Turning now to Figure 2, the
fluffer 17 is seen to comprise an outer housing which is provided with anentrance aperture 18 which, in one embodiment of the invention, may conveniently have a diameter of something between 25 and 26 cm. The air entrained polyethylene film/paper fibre balls impacts against a first plurality of impact surfaces which bearreference numerals 19 to 27 inclusive in Figures 2 and 3 and all of which lie at an angle of less than 900 to the stream of air. - Broadly, the function of the first plurality of impact surfaces is to complete, by physical impact, the separation of the polyethylene film from the paper fibres and this is accomplished by causing the material to impact against the angularly disposed impact surfaces in a more or less random, highly turbulent manner. The relatively high velocity air stream in which the material is entrained assists in this separation due to the difference between the specific gravity of the damp paper fibre balls and the polyethylene film. The relatively low air resistance of the paper fibre balls and the relatively high air resistance of the polyethylene film pieces aids in this separation.
- An
exit passage 23 is provided from the chamber defined by thefluffer 17 and leads into the first of the cascade of separator chambers which are identified in Figure 1 by the legend -SEPARATORS- and byreference numerals 29. - Each
separator chamber 29 is.as illustrated in Figure 4, and comprises a generally rectangular chamber, the first in the cascade having arectangular entrance aperture 30 and a chevronshaped exit aperture 31. - The function of each separator chamber is to provide alternate passages of high velocity (the entrance and exit apertures) and chambers of low velocity (the interior of each separator chamber 29) so as to enable the relatively heavier damp paper fibre balls to fall by gravity through a
screen 32 into'aqravity collection chamber 33 located beneath the screen. Conveniently, eachseparator chamber 29 is provided with atransparent window 34 through which the activity within the chamber may be observed. Clearly, the provision of the transparent window is optional and is not an essential feature of the invention. - In addition, each separator chamber may be provided with an
openable access door 35 to provide access to the interior of the chamber for any of a variety of purposes that will readily be apparent. - The
screen 32 in the first series of the cascade of separators will be of a mesh approximately 1 cm and will be formed in 2 sections, separated by a dividingline 32a so as to enable the .screen to be removed through theaccess door 35. - The air entrained polyethylene film/balled paper fibre material, passing through the cascade of separator chambers will maintain the relatively lighter polyethylene film in air entrainment and will permit the relatively heavier damp paper fibre balls to fall through the screen into the
collection chambers 33. Periodically, a discharge opening in the bottom of eachcollector chamber 33 will be opened to permit the accumulated paper fibre balls to fall downwardly to a point of collection which may be accomplished by any of several conventional means such as conveyors or the like. One convenient way of providing for the intermittent opening of the discharge opening in the bottom of thecollection chamber 33 is to provide aspherical plug 36 which seats in a circular opening in the bottom of thecollection chamber 33 and which may be intermittently lifted off its seat to permit the accumulated paper fibre balls to fall out through the discharge opening. - Referring to Figure 5, a convenient arrangement for lifting the
spherical plug 36 off its circular seat at the bottom of eachcollector chamber 33 is shown. Abridging member 50 extends across the upper portion of eachcollector chamber 33 and, at each end, is secured to the wall of thecollector chamber 33 by means of asmall flange 51 which may be spot welded to the wall. The lower surface of themember 50 carries abrafket 52 which, in turn, carries apulley 53 over which is entrained awire 54 which is connected, at one end, to thespherical plug 36 and, at its other end, is connected to theupper end 55 of anarm 56 which is pivotally mounted at 57 on standingstructure 58 of the apparatus. - A
longitudinal shaft 59 carries aradial cam 60. - Upon rotation of the
shaft 59, thecam 60 engages thearm 56 and causes it to move to thedotted line position 56a as a result of which thewire 54 is pulled and theball 36 is lifted off its seat to assume thedotted line position 36a. - The radial dimension of the cam 60 will determine the height to which the
spherical plug 36 is lifted, and the speed of rotation of theshaft 59 will determine the frequency at which it is lifted. It will be understood that there will be a plurality ofcams 60 equal to the number ofcollection chambers 33 and it will also be appreciated that thecams 60 can be arranged on the shaft with the same angular orientation so that all spherical plugs are lifted at the same time or they may be arranged at different angular orientations relative to the shaft so that the spherical plugs are lifted sequentially in any desired order. Furthermore, the radial extent of thecams 60 may vary so that the spherical plugs are lifted by different amounts as may be desired. - Having passed through the first five separators of the cascade, the air entrained material enters a
second fluffer 37 constructed in a manner identical to thefluffer 17 illustrated in greater detail in Figures 2 and 3. Here further impacting against a second plurality of impact surfaces takes place to further promote the physical separation of the polyethylene film from the damp paper fibre balls and, exiting from the second fluffer, the material passes through the second series of the cascade of separators identified byreference numeral 39. - By the time the air stream leaves the
final exit 40 of the last of the cascade of separator chambers, it will contain substantially pure polyethylene film and, at this point, it may be collected, passed to adryer 41 in which, by conventional means, the moisture content may be reduced to the desired level and, from the dryer,.the polyethylene film may be passed to anextruder 42 or to such other component of the apparatus as will produce a polyethylene product, suitable for recycling, in a form that can be readily shipped. The polyethylene film may be bagged, bailed, boxed or otherwise dealt with or, as illustrated in Figure 1, may be extruded into pellets, rods, bars or the like for shipment to a point of further use. - From the foregoing description, it will be apparent that an apparatus has been provided which will accept a feedstock consisting primarily of polyethylene film contaminated with paper fibres and produce a re-usable polyethylene of acceptable purity in a manner that is simple, efficient and economical of energy consumption.
- Minor modifications in the particular details of construction illustrated in the drawings will occur to those skilled in the art and such modifications and alterations are intended to be encompassed within the scope of the appended claims.
Claims (10)
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US05/849,548 US4162768A (en) | 1977-11-08 | 1977-11-08 | Apparatus for separating paper fibres from portions of polyethylene film material |
CA000331147A CA1136581A (en) | 1977-11-08 | 1979-07-04 | Apparatus for separating paper fibres from portions of polyethylene film material |
AU48994/79A AU4899479A (en) | 1977-11-08 | 1979-07-17 | Apparatus for separating paper fibres from portions of polyethylene material |
US849548 | 1986-04-08 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0002122A1 true EP0002122A1 (en) | 1979-05-30 |
EP0002122B1 EP0002122B1 (en) | 1982-02-10 |
Family
ID=27154589
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19780300612 Expired EP0002122B1 (en) | 1977-11-08 | 1978-11-08 | Method and apparatus for separating paper and fibres from portions of polyethylene film material |
Country Status (6)
Country | Link |
---|---|
US (1) | US4162768A (en) |
EP (1) | EP0002122B1 (en) |
AU (1) | AU4899479A (en) |
CA (1) | CA1136581A (en) |
DE (1) | DE2861625D1 (en) |
NO (1) | NO783756L (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0054754A2 (en) * | 1980-12-19 | 1982-06-30 | Hubert Eirich | Method of separating plastics materials from waste mixtures |
US4379748A (en) * | 1980-02-08 | 1983-04-12 | Esmil International B.V. | Method of separating paper and plastic pieces |
US4623515A (en) * | 1980-12-24 | 1986-11-18 | Organ-Fager Technology, N.V. | Process for producing fibrous and granular materials from waste |
US5246115A (en) * | 1990-08-01 | 1993-09-21 | Centro Sviluppo Settori Impiego S.R.L. | Process for separating heterogeneous plastic material into homogeneous fractions and apparatus useful to this purpose |
WO1996016779A1 (en) * | 1994-12-02 | 1996-06-06 | Brooks Thomas W | Method and apparatus of recycling previously used agricultural plastic film mulch |
US6149012A (en) * | 1997-11-17 | 2000-11-21 | Advanced Environmental Recycling Technologies, Inc. | System and method for cleaning and recovering plastic from coated fiber polywaste |
CN110065176A (en) * | 2019-06-03 | 2019-07-30 | 钟隆君 | A kind of multilayer colouring plastic grain production cleaning device |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4557800A (en) * | 1982-06-04 | 1985-12-10 | James River Corporation | Process of forming a porous cellulosic paper from a thermal treated cellulosic non-bonding pulp |
US5268074A (en) * | 1990-03-27 | 1993-12-07 | Advanced Environmental Recycling Technologies, Inc. | Method for recycling polymeric film |
US5084135A (en) * | 1990-03-27 | 1992-01-28 | Advanced Environmental Recycling Technologies, Inc. | Recycling plastic coated paper product waste |
DE4042222A1 (en) * | 1990-12-29 | 1992-07-02 | Pwa Industriepapier Gmbh | METHOD FOR REPROCESSING THERMOPLAST COATED PACKAGING MATERIALS AND THERMOPLASTIC MATERIAL FOR FURTHER PROCESSING |
CA2107239C (en) * | 1991-03-21 | 2004-05-25 | Joe G. Brooks | Method for recycling plastic coated paper product waste and polymeric film |
US5285973A (en) * | 1992-07-15 | 1994-02-15 | Advanced Environmental Recycling Technologies, Inc. | Close tolerance shredder |
US5540244A (en) * | 1993-12-07 | 1996-07-30 | Advanced Environmental Recycling Technologies, Inc. | Method and apparatus for cleaning and recycling post-consumer plastic films |
CA2323825C (en) * | 2000-10-19 | 2008-01-08 | Eco-Shred Ltd. | Paper separation and singulation apparatus and method |
CN103263075B (en) * | 2013-06-11 | 2015-08-12 | 红塔烟草(集团)有限责任公司 | High efficiency energy saving leaf beating wind separating new technology and equipment |
CN107485777B (en) * | 2017-09-06 | 2020-12-15 | 乐普(北京)医疗器械股份有限公司 | Preparation method of crystal-controllable drug balloon catheter |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
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GB659531A (en) * | 1949-06-14 | 1951-10-24 | John Graham Campbell | Apparatus for sorting out powders according to particle size |
GB699386A (en) * | 1951-08-01 | 1953-11-04 | Weston David | Classifier for material reduction mills |
US3447678A (en) * | 1967-04-20 | 1969-06-03 | Donald L Henry | Method for separating expanded perlite with minimum particle breakage |
US3856217A (en) * | 1973-06-04 | 1974-12-24 | Garbalizer Corp | Combination shredder and air-classification equipment |
FR2279471A1 (en) * | 1974-07-22 | 1976-02-20 | Black Clawson Fibreclaim Inc | PROCESS FOR RECOVERING PLASTIC MATERIAL MIXED WITH HOUSEHOLD WASTE |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
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US1403399A (en) * | 1921-03-31 | 1922-01-10 | Frist Robert Porter | Stemmer for deciduous fruit |
US3250389A (en) * | 1965-01-28 | 1966-05-10 | Systems Engineering And Mfg Co | Line sifter |
US3484948A (en) * | 1967-08-09 | 1969-12-23 | John Campbell Whelan | Apparatus for exchanging heat between a gas and a particulate matter |
US3836085A (en) * | 1971-03-18 | 1974-09-17 | V Brown | Tower extractor for municipal wastes |
BE794381A (en) * | 1972-02-04 | 1973-05-16 | Ruggero Levi Detto Acobas | METHOD AND DEVICE FOR RECOVERING CELLULOSE FIBERS AND PLASTIC MATERIAL FROM PLASTIC COATED PAPERS AND CARDBOARDS |
US3929293A (en) * | 1973-05-16 | 1975-12-30 | Pennsylvania Crusher Corp | Shredder crusher material reducer |
-
1977
- 1977-11-08 US US05/849,548 patent/US4162768A/en not_active Expired - Lifetime
-
1978
- 1978-11-08 EP EP19780300612 patent/EP0002122B1/en not_active Expired
- 1978-11-08 DE DE7878300612T patent/DE2861625D1/en not_active Expired
- 1978-11-08 NO NO783756A patent/NO783756L/en unknown
-
1979
- 1979-07-04 CA CA000331147A patent/CA1136581A/en not_active Expired
- 1979-07-17 AU AU48994/79A patent/AU4899479A/en not_active Abandoned
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB659531A (en) * | 1949-06-14 | 1951-10-24 | John Graham Campbell | Apparatus for sorting out powders according to particle size |
GB699386A (en) * | 1951-08-01 | 1953-11-04 | Weston David | Classifier for material reduction mills |
US3447678A (en) * | 1967-04-20 | 1969-06-03 | Donald L Henry | Method for separating expanded perlite with minimum particle breakage |
US3856217A (en) * | 1973-06-04 | 1974-12-24 | Garbalizer Corp | Combination shredder and air-classification equipment |
FR2279471A1 (en) * | 1974-07-22 | 1976-02-20 | Black Clawson Fibreclaim Inc | PROCESS FOR RECOVERING PLASTIC MATERIAL MIXED WITH HOUSEHOLD WASTE |
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4379748A (en) * | 1980-02-08 | 1983-04-12 | Esmil International B.V. | Method of separating paper and plastic pieces |
EP0054754A2 (en) * | 1980-12-19 | 1982-06-30 | Hubert Eirich | Method of separating plastics materials from waste mixtures |
EP0054754A3 (en) * | 1980-12-19 | 1983-10-19 | Hubert Eirich | Method of separating plastics materials from waste mixtures |
US4623515A (en) * | 1980-12-24 | 1986-11-18 | Organ-Fager Technology, N.V. | Process for producing fibrous and granular materials from waste |
US5246115A (en) * | 1990-08-01 | 1993-09-21 | Centro Sviluppo Settori Impiego S.R.L. | Process for separating heterogeneous plastic material into homogeneous fractions and apparatus useful to this purpose |
WO1996016779A1 (en) * | 1994-12-02 | 1996-06-06 | Brooks Thomas W | Method and apparatus of recycling previously used agricultural plastic film mulch |
US6149012A (en) * | 1997-11-17 | 2000-11-21 | Advanced Environmental Recycling Technologies, Inc. | System and method for cleaning and recovering plastic from coated fiber polywaste |
CN110065176A (en) * | 2019-06-03 | 2019-07-30 | 钟隆君 | A kind of multilayer colouring plastic grain production cleaning device |
CN110065176B (en) * | 2019-06-03 | 2021-03-26 | 浙江同发塑机有限公司 | Multilayer plastic granules production belt cleaning device of coloring |
CN112959543A (en) * | 2019-06-03 | 2021-06-15 | 钟隆君 | Multi-layer coloring plastic particle production cleaning system and cleaning method |
CN112959543B (en) * | 2019-06-03 | 2022-10-18 | 伟亨实业(深圳)有限公司 | Multi-layer coloring plastic particle production cleaning system and cleaning method |
Also Published As
Publication number | Publication date |
---|---|
CA1136581A (en) | 1982-11-30 |
NO783756L (en) | 1979-05-09 |
US4162768A (en) | 1979-07-31 |
AU4899479A (en) | 1981-01-22 |
DE2861625D1 (en) | 1982-03-18 |
EP0002122B1 (en) | 1982-02-10 |
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